CN101185844A - Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device - Google Patents
Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device Download PDFInfo
- Publication number
- CN101185844A CN101185844A CNA2007100530915A CN200710053091A CN101185844A CN 101185844 A CN101185844 A CN 101185844A CN A2007100530915 A CNA2007100530915 A CN A2007100530915A CN 200710053091 A CN200710053091 A CN 200710053091A CN 101185844 A CN101185844 A CN 101185844A
- Authority
- CN
- China
- Prior art keywords
- ionization
- reaction
- industrial boiler
- flue gas
- fathering
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Abstract
The invention relates to an industrial boiler flue gas pollution governing method and an apparatus with a dual catalysis of ionization and electron accelerating reaction; the industrial boiler waste gas is processed by a cooling tower 1, a bag filter 2, an air control valve 3, an ionization machine 4, a reaction tower 5, an electronic accelerator 6, a bag filter 7, a draft fan 8, and a chimney 9. The invention has the advantages that the method and the apparatus are better than a pure electron beam technique in Japan; the overall purifying rate prediction in urban air purification can reach 98%; wastes can be utilized effectively and circularly; a great deal of carbon dioxide exhaustion, an aggravation of the greenhouse effect and a destruction of the ecological environment are avoided.
Description
Technical field
The present invention relates to the Industrial Boiler technical field of waste gas treatment, a kind of specifically ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device.
Background technology
Administering the Industrial Boiler smoke pollution is world-famous puzzle, and best improvement method is all being sought, traditional improvement method by each state: the one, and in the boiler of burning, add agstone and neutralize, both influenced boiler efficiency, the pollution treatment effect is not good yet; The 2nd, neutralize in the flue cellar or in the reaction tower with white lime water liquid spray, the pollution treatment effect is also undesirable, and floor space Da Yi causes secondary pollution.
In recent years have both at home and abroad and utilize ionization, electron beam to administer dusty gas respectively, desulfurization degree reaches 80%, and denitrification percent reaches 70%, does not all reach national specified discharge standard.But started the beginning of administering dusty gas with modern high technology, European industrially developed country has the ionization of the high pressure pulse discharge of employing to administer dusty gas, reaches nanosecond interpulse period, and China's electronic original part far is not up to the standard.
Summary of the invention
The objective of the invention is to develop a kind of Industrial Boiler, the toxic emission rate is very low, and waste gas obtains recycling ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device.
Ionization of the present invention, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method, comprise: at first make Industrial Boiler waste gas enter cooling tower 1, under the cooperation of spray equipment, big grain dust is settled down with temperature, and remaining gas enters deduster 2, dispels favourable ionization machine 4 ionization of particle dust, about 20,000 volts of ionization voltages, make some materials and carbon dioxide become solid state powder with sulphur, nitrogen ionization charing, in ionization process if the oxygen supply deficiency, 3 oxygen supplys of available adjustment valve.Sulphur and nitrogen that obstinate escape is fallen are activated under the high voltage electric field effect, resolve into the unimolecule structure, produce a large amount of ozone in the time of ionization.Ozone is a kind of strong oxidizer, plays catalysis in course of reaction, enters reaction tower 5 with air-flow, at normal temperatures and pressures ammonia is added reaction tower 5 simultaneously, generates ammonium sulfate, ammonium nitrate and other material.After 6 catalysis of electronics accelerating reactor, the accelerated reaction cohesive process makes combination reaction more become perfect, enters comminutor by deduster 7 collections again and makes granulated fertilizer, and clean gas is discharged through chimney.
Ionization of the present invention, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution device, comprise: cooling tower 1, sack cleaner 2, air control valve 3, ionization machine 4, reaction tower 5, electron accelerator 6, sack cleaner 7, air-introduced machine 8, chimney 9 connect with pipeline between each device.
Ionization machine 4 is applicant's patent applied for " shell and tube industrial gas volume ionization clearing machines ", and application number is 200620099212.0.
Electron accelerator 6 is applicant's patent applied for " breaking of electronics accelerated reaction machines ", and application number is 200620099211.6.
The advantage of ionization of the present invention, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device is: the simple electron beam technology that is better than Japan, effect in urban air purifies, estimate that the gross decontamination rate can reach 98%, refuse can be effectively recycling, avoids a large amount of dischargings, aggravation greenhouse effects, the destruction ecological environment of carbon dioxide.
Description of drawings
Accompanying drawing is the structural representation of ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution device.
The specific embodiment
With reference to the accompanying drawings, at first make Industrial Boiler waste gas enter cooling tower 1, under the cooperation of spray equipment, big grain dust is settled down with temperature, and remaining gas enters deduster 2, dispels favourable ionization machine 4 ionization of particle dust, about 20,000 volts of ionization voltages, make some materials and carbon dioxide become solid state powder with sulphur, nitrogen ionization charing, in ionization process if the oxygen supply deficiency, 3 oxygen supplys of available adjustment valve.Sulphur and nitrogen that obstinate escape is fallen are activated under the high voltage electric field effect, resolve into the unimolecule structure, produce a large amount of ozone in the time of ionization.Ozone is a kind of strong oxidizer, plays catalysis in course of reaction, enters reaction tower 5 with air-flow, at normal temperatures and pressures ammonia is added reaction tower 5 simultaneously, generates ammonium sulfate, ammonium nitrate and other material.After 6 catalysis of electronics accelerating reactor, the accelerated reaction cohesive process makes combination reaction more become perfect, enters comminutor by deduster 7 collections again and makes granulated fertilizer, and clean gas is discharged through chimney.
Claims (2)
1. ionization; electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method; it is characterized in that: at first make Industrial Boiler waste gas enter cooling tower (1); under the cooperation of spray equipment; big grain dust is settled down with temperature; remaining gas enters deduster (2); dispel the favourable ionization machine of particle dust (4) ionization; about 20,000 volts of ionization voltages; make some materials and carbon dioxide and sulphur; nitrogen ionization charing becomes solid state powder; in ionization process if the oxygen supply deficiency; available adjustment valve (3) oxygen supply; sulphur and nitrogen that obstinate escape is fallen are activated under the high voltage electric field effect; resolve into the unimolecule structure; produce a large amount of ozone in the time of ionization; ozone is a kind of strong oxidizer; in course of reaction, play catalysis; enter reaction tower (5) with air-flow; at normal temperatures and pressures ammonia is added simultaneously reaction tower (5); generate ammonium sulfate; ammonium nitrate and other material; after electronics accelerating reactor (6) catalysis; it is perfect that the combination reaction that makes the accelerated reaction cohesive process more becomes, and enters comminutor by deduster (7) collection again and make granulated fertilizer, and clean gas is discharged through chimney.
2. an ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution device, it is characterized in that: cooling tower (1), sack cleaner (2), air control valve (3), ionization machine (4), reaction tower (5), electron accelerator (6), sack cleaner (7), air-introduced machine (8), chimney (9) connect with pipeline between each device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007100530915A CN101185844A (en) | 2007-08-30 | 2007-08-30 | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007100530915A CN101185844A (en) | 2007-08-30 | 2007-08-30 | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101185844A true CN101185844A (en) | 2008-05-28 |
Family
ID=39478591
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2007100530915A Pending CN101185844A (en) | 2007-08-30 | 2007-08-30 | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101185844A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101648098B (en) * | 2008-08-14 | 2011-06-15 | 徐志远 | Device and method for purifying and recycling oil, water and dust in flue gas |
CN104888587A (en) * | 2015-06-29 | 2015-09-09 | 李梦燕 | Method for processing garbage incineration waste gases |
CN113149354A (en) * | 2021-04-23 | 2021-07-23 | 扬州华大锅炉有限公司 | Sewage discharge treatment process for thermal system of hot water boiler |
-
2007
- 2007-08-30 CN CNA2007100530915A patent/CN101185844A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101648098B (en) * | 2008-08-14 | 2011-06-15 | 徐志远 | Device and method for purifying and recycling oil, water and dust in flue gas |
CN104888587A (en) * | 2015-06-29 | 2015-09-09 | 李梦燕 | Method for processing garbage incineration waste gases |
CN113149354A (en) * | 2021-04-23 | 2021-07-23 | 扬州华大锅炉有限公司 | Sewage discharge treatment process for thermal system of hot water boiler |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101869800B (en) | Method and system for purifying flue gas generated by incinerating waste materials | |
CN102015070B (en) | System for treating discharge gas and method of removing mercury from discharge gas | |
CN202289839U (en) | House refuse incineration smoke purifying system | |
CN101785969B (en) | Method of flue gas purification and system thereof | |
CN103432887B (en) | A kind of waste incinerated smoke purification system and technique | |
CN102120130A (en) | Complete set of device and method for treating tail gas from sludge incineration through semidry method | |
CN101822942B (en) | Wet purification method for dioxin and heavy metals in solid waste incineration gas | |
CN106861415B (en) | Flue gas purification system and method | |
CN101357290A (en) | Method and system of controlling dioxin discharge in flue gas by duty-cycle operation of sulphur-containing inhibitor | |
CN203886406U (en) | Tail gas purification device of circulating fluid bed garbage incinerator | |
CN101579599A (en) | Novel process for treating fermentation waste gas of amino acid by utilizing biofilter | |
CN102091515A (en) | Method for purifying air with high-energy ions | |
CN107485999A (en) | The processing method of flue gas of refuse burning | |
CN104976625B (en) | A kind of processing system and processing method of the organic phosphorus waste liquid of high concentration | |
CN201899980U (en) | Complete device for treating sludge incineration tail gas in semidry method | |
CN111359422A (en) | Efficient dry deacidification device and method for waste incineration flue gas | |
CN101850214B (en) | Plasma-catalytic oxidation refuse burning and cracking tail gas purification device | |
CN113587117B (en) | System and method for innocent treatment of sludge | |
CN107596903A (en) | Method for capturing carbon dioxide in flue gas by using supergravity carbonating device | |
CN101185844A (en) | Ionization, electronic accelerated reaction dual catalytic fathering industrial boiler flue gas pollution method and device | |
CN106178877A (en) | A kind of coke oven flue waste gas purification waste heat recovery apparatus and technique | |
CN203653400U (en) | Sludge drying and incineration power generation integrated system | |
CN205640929U (en) | Waste incineration treatment system | |
CN107551779A (en) | The processing unit of flue gas of refuse burning | |
CN101915423B (en) | Refuse burning system and method with functions of deacidifying flue gas and retarding dioxin generation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Open date: 20080528 |